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WO2013146103A1 - Refrigerating cycle device - Google Patents

Refrigerating cycle device Download PDF

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Publication number
WO2013146103A1
WO2013146103A1 PCT/JP2013/055773 JP2013055773W WO2013146103A1 WO 2013146103 A1 WO2013146103 A1 WO 2013146103A1 JP 2013055773 W JP2013055773 W JP 2013055773W WO 2013146103 A1 WO2013146103 A1 WO 2013146103A1
Authority
WO
WIPO (PCT)
Prior art keywords
refrigerant
refrigeration cycle
cycle apparatus
connection pipe
pipe
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Ceased
Application number
PCT/JP2013/055773
Other languages
French (fr)
Japanese (ja)
Inventor
坪江 宏明
横関 敦彦
福治 塚田
中山 進
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Hitachi Global Life Solutions Inc
Original Assignee
Hitachi Appliances Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Hitachi Appliances Inc filed Critical Hitachi Appliances Inc
Priority to CN201380008246.7A priority Critical patent/CN104094069B/en
Priority to EP13769631.6A priority patent/EP2840335B1/en
Priority to US14/376,804 priority patent/US10066859B2/en
Publication of WO2013146103A1 publication Critical patent/WO2013146103A1/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B41/00Fluid-circulation arrangements
    • F25B41/40Fluid line arrangements
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B41/00Fluid-circulation arrangements
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B13/00Compression machines, plants or systems, with reversible cycle
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2400/00General features or devices for refrigeration machines, plants or systems, combined heating and refrigeration systems or heat-pump systems, i.e. not limited to a particular subgroup of F25B
    • F25B2400/12Inflammable refrigerants
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2500/00Problems to be solved
    • F25B2500/01Geometry problems, e.g. for reducing size

Definitions

  • the present invention relates to a refrigeration cycle apparatus such as an air conditioner or a refrigerator using a refrigeration cycle, and particularly relates to one using R32 (difluoromethane) as a refrigerant used in the refrigeration cycle.
  • a refrigeration cycle apparatus such as an air conditioner or a refrigerator using a refrigeration cycle
  • R32 difluoromethane
  • refrigerant R410A can improve the efficiency of the refrigerating and air-conditioning equipment, and can reduce the amount of carbon dioxide generated during power generation by reducing the power consumption. In addition, it contributes to the prevention of global warming by reducing refrigerant discharge by measures against refrigerant leakage.
  • the refrigerant R410A is a refrigerant having a high GWP (global warming potential)
  • a refrigerant R32 can be considered as the refrigerant.
  • the refrigerant R32 has a slightly flammable characteristic, and it is preferable to reduce the amount of refrigerant sealed in the refrigeration cycle as much as possible in order to reduce the amount of refrigerant leakage in the event of refrigerant leakage.
  • connection pipe refrigerant pipe
  • the pipe diameter of the connection pipe (refrigerant pipe) connecting the outdoor unit and the indoor unit can be reduced by converting the refrigerant R410A to the refrigerant R32, not only the amount of refrigerant to be sealed can be reduced, but also the connection pipe It is possible to reduce the amount of copper used as a material, and it is also possible to improve the workability of connection pipes during construction of air conditioners and the like.
  • Patent Document 1 Japanese Patent Application Laid-Open No. 2001-248941
  • Patent Document 2 Japanese Patent Application Laid-Open No. 2002-89978
  • the diameters of the liquid side connection pipe and the gas side connection pipe are set in consideration of the conversion from the refrigerant R22, which is an HCFC refrigerant, to the refrigerant R32.
  • the connection pipe diameter is not always sufficient.
  • the refrigerant R410A is a comparison between the refrigerant R410A and refrigerant R32, which are currently widely used, is as follows.
  • the following piping diameter is generally used.
  • the outer diameter of the liquid side connecting pipe is 1/4 inch (6.35 mm)
  • the outer diameter of the gas side connecting pipe is 1/2 inch ( 12.7 mm)
  • the outer diameter of the liquid side connection pipe is 3/8 inch (9.53 mm)
  • the gas side connection pipe The outer diameter of the tube is 5/8 inch (15.88 mm).
  • the rated refrigeration capacity is 4.5 kW or more and less than 7.1 kW.
  • the diameters of the liquid side connection pipe and the gas side connection pipe are not different from those used in the refrigerant R410A.
  • the rated refrigeration capacity exceeds 7.1 kW and is equal to or less than 14.0 kW, only the liquid side connection pipe is reduced in diameter.
  • An object of the present invention is to obtain a refrigeration cycle apparatus that can suppress a decrease in efficiency while using a refrigerant having a low global warming potential (GWP) and that can also reduce the pipe diameter of a connection pipe.
  • GWP global warming potential
  • the present invention includes a compressor, a heat source unit side heat exchanger, a first expansion device, a liquid side connection pipe, a second expansion device, a use side heat exchanger, and a gas side connection pipe.
  • the refrigerant used in the refrigeration cycle is R32
  • Pipe outer diameters of the liquid side connection pipe and the gas side connection pipe are: (D 0 -1) / 8 inches (where "D 0/8 inches” is a connection pipe outer diameter in the case of using the refrigerant R410A) and, and the range of the D 0 in the liquid connection pipe " 2 ⁇ D 0 ⁇ 4 ”, and in the gas connection pipe, the range of D 0 is“ 3 ⁇ D 0 ⁇ 8 ”.
  • the D 0 is 3 (that is, the pipe diameter is 1/4 inch) in the liquid connection pipe, and the D 0 is 5 in the gas connection pipe. (i.e., the pipe diameter of 1/2 inch) and, in a range of less than 7.1kW rated cooling capacity from 3.6kW, the D 0 2.5 (i.e. pipe diameter 3/16 inch) in the liquid connection pipe In the gas side connection pipe, the D 0 is preferably 4 (that is, the pipe diameter is 3/8 inch).
  • the compressor, the heat source unit side heat exchanger, the first expansion device, the liquid side connection piping, the second expansion device, the use side heat exchanger, and the gas side connection piping are sequentially connected.
  • the refrigerant used in the refrigeration cycle is R32
  • the liquid side connection pipe and the pipe outer diameter of the gas side connection pipe are: D 0/8 inches
  • the range of D 0 is “1 ⁇ D 0 ⁇ 3”
  • the range of D 0 is “2 ⁇ D 0 ⁇ 7”.
  • the liquid connection piping the D 0 2 i.e. pipe diameter is 1/4 inches
  • the D 0 is the gas connection pipe 4 (i.e., the pipe diameter of 1/2 inch)
  • the liquid connecting the D 0 1.5 i.e. pipe diameter 3/16 inch
  • the D 0 is preferably 3 (that is, the pipe diameter is 3/8 inch).
  • the amount of refrigerant R32 enclosed in the refrigeration cycle apparatus is equal to the amount of refrigerant R410A enclosed in the same specification refrigeration cycle apparatus using R410A as the refrigerant and having the same rated refrigeration capacity. It is better to set a smaller amount.
  • the amount of refrigerant R32 enclosed in the refrigeration cycle apparatus is W 1 [kg]
  • the refrigeration cycle apparatus has a rated refrigeration capacity of Qc [kW]
  • the refrigeration cycle having the same rated refrigeration capacity Qc [kW] using the refrigerant R410A.
  • the refrigerant filling amount in the apparatus is W 0 [kg]
  • the refrigerant filling amount W 1 to the refrigeration cycle apparatus using the refrigerant R32 is For Qc ⁇ 7.1 kW, (0.011Qc + 0.60) W 0 ⁇ W 1 ⁇ W 0
  • Qc ⁇ 7.1 kW (0.030Qc + 0.71) W 0 ⁇ W 1 ⁇ W 0 It is preferable to set in the range.
  • a refrigeration cycle apparatus that can suppress a decrease in efficiency while using a refrigerant having a low global warming potential (GWP) and that can also reduce the pipe diameter of the connection pipe.
  • GWP global warming potential
  • Example 1 of the refrigerating-cycle apparatus of this invention The figure explaining the connection pipe diameter and refrigerant
  • coolant R32 WHEREIN The diagram which shows refrigerant
  • coolant amount ratio refrigerant
  • FIG. 1 is a cycle system diagram illustrating Example 1 of the refrigeration cycle apparatus of the present invention
  • FIG. 2 is a refrigeration cycle apparatus using refrigerants R410A and R32 serving as the same COP (rated refrigeration capacity 7.1 kW, 12.5 kW).
  • FIG. 3 is a diagram for explaining the connection pipe diameter and the refrigerant amount ratio in FIG. 3.
  • FIG. 3 shows the connection pipe diameter in the refrigeration cycle apparatus (rated refrigeration capacity 3.6 kW, 5.6 kW) using the refrigerants R410A and R32, which are similar COPs. It is a figure explaining refrigerant
  • FIG. 1 shows an air conditioner as a refrigeration cycle apparatus, in which an outdoor unit 40 and an indoor unit 20 are connected by a liquid side connection pipe 7 and a gas side connection pipe 8.
  • 1 is a compressor (sealed compressor)
  • 2 is a four-way valve
  • 3 is a heat source side heat exchanger
  • 4 is a first expansion device
  • 6 is a liquid side blocking valve
  • 9 is a gas.
  • the side stop valve 10 is an accumulator.
  • 21 is a second expansion device
  • 22 is a use side heat exchanger.
  • the compressor 1, the heat source device side heat exchanger 3, the first expansion device 4, the liquid side connection piping 7, the second expansion device 21, the use side heat exchanger 22, the gas side connection piping 8, etc. are sequentially connected piping. (Refrigerant piping) is connected and the refrigerating cycle apparatus (an air conditioner in a present Example) is comprised.
  • the gas refrigerant compressed by the compressor 1 to become high temperature and pressure is discharged from the compressor 1 together with refrigeration oil, and the gas refrigerant passes through the four-way valve 2 to exchange heat with the heat source unit. It flows into the vessel 3, where it exchanges heat and condensates.
  • the condensed and liquefied refrigerant passes through the fully expanded first expansion device 4, and then passes through the blocking valve 6 and the liquid side connection pipe 7, and is sent to the indoor unit 20.
  • the liquid refrigerant sent to the indoor unit 20 flows into the second expansion device 21, where it is decompressed to become a low-pressure two-phase state, and exchanges heat with the utilization side medium such as air in the utilization side heat exchanger 22. Evaporate and gasify.
  • the gas refrigerant passes through the gas side connection pipe 8 and the blocking valve 9 and returns to the compressor 1 again via the four-way valve 2.
  • the surplus refrigerant is stored in the accumulator 10 so that the operating pressure and temperature of the refrigeration cycle are maintained in a normal state.
  • the gas refrigerant compressed into the high temperature and high pressure by the compressor 1 is discharged from the compressor 1 together with the refrigerating machine oil.
  • the gas refrigerant flows to the blocking valve 9 side by the four-way valve 2 and flows into the use side heat exchanger 22 of the indoor unit 20 through the gas side connection pipe 8.
  • the gas refrigerant is condensed and liquefied by exchanging heat with a use side medium such as air.
  • the condensed and liquefied refrigerant is depressurized by the first expansion device 4 through the liquid side connection pipe 7 and the blocking valve 6, and is evaporated by exchanging heat with a heat source medium such as air or water in the heat source unit side heat exchanger 3. ⁇ Gasify.
  • the evaporated and gasified refrigerant returns to the compressor 1 again through the four-way valve 2.
  • the refrigeration cycle apparatus of the present embodiment uses R32 as a refrigerant, and the outer diameters of the liquid side connection pipe 7 and the gas side connection pipe 8 are made larger than those of the refrigeration cycle apparatus having the same rated refrigeration capacity using the refrigerant R410A.
  • One rank is set thin.
  • the setting of the pipe outer diameter of the connection pipes 7 and 8 will be described in detail. In the present embodiment, the case of cooling operation in which a larger amount of refrigerant is required will be described.
  • the refrigerant amount is, for example, the internal volume of the refrigeration cycle (the internal volume of the compressor 1, the heat source machine side heat exchanger 3, the liquid side connection pipe 7, the use side heat exchanger 22, the gas side connection pipe 8, the accumulator 10, etc.) It can be determined according to the density of the refrigerant. In addition, the amount of refrigerant dissolved in the refrigerating machine oil sealed in the compressor 1 and a refrigerating cycle in which a receiver is installed between the first expansion device 4 and the liquid side blocking valve 6. In the apparatus, it is more preferable to determine the refrigerant amount in consideration of the internal volume of the receiver.
  • FIG. 2 shows the refrigerant amount of the refrigeration cycle apparatus using the refrigerant R32, which is the minimum required to be equivalent to the COP of the refrigeration cycle apparatus using the refrigerant R410A, and the refrigeration cycle apparatus using the refrigerant R410A. It is the figure shown with the refrigerant
  • the length of the connecting pipes 7 and 8 is the maximum connecting pipe length (chargeless maximum pipe length) that can be handled only by the amount of refrigerant sealed at the time of shipment from the factory, and is 30 m when the rated refrigeration capacity is 7.1 kW and 12.5 kW. It is.
  • connection pipes 7 and 8 are longer than the chargeless maximum pipe length, it can be dealt with by adding a predetermined refrigerant amount according to the length of the pipe that exceeds the chargeless maximum pipe length at the time of construction. .
  • the pipe outer diameters of the connection pipes 7 and 8 of the refrigeration cycle apparatus using the refrigerant R32 are the pipe outer diameters of the connection pipes 7 and 8 of the refrigeration cycle apparatus using the refrigerant R410A.
  • Is “D 0/8 inch” however, in this embodiment, the range of D 0 is “2 ⁇ D 0 ⁇ 4” in the liquid connection pipe 7 and “3 ⁇ D in the gas connection pipe 8”. 0 ⁇ 8 ”
  • the outer diameter of the pipe is one rank smaller than this, ie,“ (D 0 ⁇ 1) / 8 inch ”.
  • the pipe outer diameters of the connection pipes 7 and 8 are generally 5/8 inch (15.88 mm) for the gas side connection pipe 8 and the liquid side connection pipe 7 for the refrigeration cycle apparatus using the refrigerant R410A. Since a 3/8 inch (9.53 mm) one is used, it is assumed that the above-mentioned tube outer diameter is also used in the description of FIG.
  • the pipe outer diameters of the connection pipes 7 and 8 are larger than the pipe outer diameters of the connection pipes 7 and 8 in the refrigeration cycle apparatus using the refrigerant R410A.
  • the following effects can be obtained by setting the 1 rank narrower. That is, the table in FIG. 2 shows that the COP is equivalent to the COP of the refrigeration cycle apparatus using the refrigerant R410A, so that the amount of copper used can be reduced and the connection piping at the time of construction can be reduced without degrading the performance of the refrigeration air conditioning equipment. A refrigeration cycle apparatus with improved workability can be obtained.
  • the amount of power when using refrigeration and air-conditioning equipment is the same as when using R410A, so low GWP (global warming potential) is achieved without increasing the amount of carbon dioxide emissions when using power accompanying power generation.
  • the refrigerant R32 is used, a refrigeration cycle apparatus effective for preventing global warming can be obtained.
  • the pipe outer diameter of the connection pipes 7 and 8 it is possible to reduce the amount of copper used as the material for the connection pipes, and also to improve the workability of the connection pipes during construction of refrigeration and air conditioning equipment. A refrigeration cycle apparatus that can be realized can be obtained.
  • the rated refrigeration capacities of 7.1 kW and 12.5 kW are described.
  • the refrigeration cycle apparatus having the rated refrigeration capacities between them also has a gas side connection pipe diameter and a liquid side connection pipe. The diameter is the same as that shown in FIG.
  • FIG. 3 shows a refrigeration cycle using the refrigerant R32, which is at least required to be equivalent to the COP of the refrigeration cycle apparatus using the refrigerant R410A in the refrigeration cycle apparatuses having the rated refrigeration capacities of 3.6 kW and 5.6 kW. It is a figure which shows the refrigerant
  • the length of the connection pipes 7 and 8 is 20 m which is the maximum connection pipe length (chargeless maximum pipe length) that can be handled only by the amount of refrigerant sealed at the time of shipment from the factory.
  • the pipe outer diameters of the connection pipes 7 and 8 of the refrigeration cycle apparatus using the refrigerant R32 are the pipe outer diameters of the connection pipes 7 and 8 of the refrigeration cycle apparatus using the refrigerant R410A.
  • connection pipes 7 and 8 have a pipe outer diameter that is one rank narrower in the gas side connection pipe 8 ((D 0 ⁇ 1 ) / 8 inch), the gas side connecting pipe 8 is 3/8 inch (9.53 mm).
  • the outer diameter of the pipe is 1/8 inch (3.18 mm) in the refrigeration cycle apparatus using the refrigerant R32.
  • the pressure loss in the liquid side connection pipe 7 becomes excessive depending on the refrigerant flow rate, and the adjustment range of the refrigerant side flow path resistance in the second expansion device 21 is increased. In some cases, the suction pressure of the compressor 1 falls outside the operating range of the compressor 1, which may reduce the reliability of the refrigeration cycle apparatus.
  • the diameter of the liquid side connection pipe 7 is expressed by “(D 0 ⁇ 1) / 8”, the D 0 is 2.5 (in this case, the outer diameter of the liquid side connection pipe 7 is 1). .5 / 8 (3/16) inch).
  • the diameter of the connection pipe 7 and 8, the outer diameter of the connection pipe 7 and 8 of the refrigeration cycle apparatus using the refrigerant R410A is "D 0/8 inches", this as a reference
  • the connection pipe diameter in the refrigeration cycle apparatus using the refrigerant R32 of the example is expressed by the above “(D 0 ⁇ 1) / 8 inch” or “(D 0 ⁇ 1) / 16 inch”.
  • connection pipe diameter in the refrigeration cycle apparatus using the refrigerant R32 is expressed without using the pipe outer diameters of the connection pipes 7 and 8 of the refrigeration cycle apparatus using the refrigerant R410A as “D 0/8 ”, (However, in this case, the range of D 0 is “1 ⁇ D 0 ⁇ 3” in the liquid connection pipe 7 and “2 ⁇ D 0 ⁇ 7” in the gas connection pipe 8). .
  • the D 0 in the range of the rated refrigeration capacity shown in FIG. 2 from 7.1 kW to 12.5 kW, in the liquid connection pipe 7, the D 0 is 2 (that is, the pipe diameter is 1/4 inch), and the gas connection pipe 8 Then, the D 0 is 4 (that is, the pipe diameter is 1/2 inch). Further, in the range of less than 7.1kW from the rated cooling capacity is 3.6kW shown in FIG. 3, the D 0 be expressed as the D 0 in the liquid connection pipe 7 is 1.5 ( “D 0/16" is 3) (that is, the pipe diameter is 3/16 inch), and in the gas side connection pipe 8, the D 0 is 3 (that is, the pipe diameter is 3/8 inch).
  • 3/16 inch thicker than 1/8 inch is used as the liquid side connection pipe 7 of the refrigeration cycle device using the refrigerant R32, so that the reliability of the refrigeration cycle device is improved.
  • the outer diameters of the connecting pipes 7 and 8 can be reduced without lowering the performance of the refrigerating and air-conditioning equipment.
  • the amount of copper pipe used can be reduced and the workability of connecting pipes during construction can be improved, and since a low-GWP refrigerant R32 is used, a refrigeration cycle apparatus effective for preventing global warming can be obtained. Can do.
  • the rated refrigeration capacities of 3.6 kW and 5.6 kW are described, but a refrigeration cycle apparatus having a rated refrigeration capacity between these, and a rating of more than 5.6 kW and less than 7.1 kW Also in the refrigeration cycle apparatus having the refrigeration capacity, the gas side connection pipe diameter and the liquid side connection pipe diameter are the same as those shown in FIG.
  • the outer diameter of the gas-side connecting pipe 8 is 3/8 inch.
  • the pipe outer diameter of the side connection pipe 7 it is preferable to adopt 3/16 inch.
  • FIG. 4 is a diagram illustrating a refrigerant amount ratio (refrigerant amount ratio at which COP is equivalent) with respect to the rated refrigeration capacity in a refrigeration cycle apparatus using refrigerant R32
  • FIG. 5 is a refrigeration cycle using refrigerants R410A and R32.
  • the apparatus it is a figure explaining the COP ratio of R410A standard when the amount of refrigerant
  • Example 1 the connecting pipes 7 and 8 of the refrigeration cycle apparatus using the refrigerant R32 have a pipe outer diameter that is one rank lower than that of the refrigeration cycle apparatus using the refrigerant R410A.
  • the amount of refrigerant (upper limit value and lower limit value) sealed in the refrigeration cycle apparatus using the refrigerant R32 will be described with reference to FIG.
  • FIG. 4 shows the relationship between the refrigerant amount ratios in the refrigeration cycle apparatus using the refrigerant R32 and a COP equivalent to that of the refrigeration cycle apparatus using the refrigerant R410A.
  • the horizontal axis represents the rated refrigeration capacity, and the vertical axis represents the R410A.
  • the refrigerant amount ratio is based on the refrigerant amount.
  • FIG. 4 is a diagram in which the refrigerant amount ratio in which the COPs shown in FIGS. 2 and 3 described above are equivalent is plotted. A straight line connecting the plotted points indicates the lower limit value of the refrigerant amount ratio necessary to be the same as the COP of the refrigeration cycle apparatus using the refrigerant R410A.
  • the pipe outer diameter of the connection pipes 7 and 8 of the refrigeration cycle apparatus using the refrigerant R32 is “(D o ⁇ 1) / 8 inch” (for example, gas side connection) when the rated refrigeration capacity is 7.1 kW or more.
  • the pipe diameter is set to 4/8 inch, and the liquid side connection pipe diameter is set to 2/8 inch).
  • the gas side connection pipe 8 is the “(D o ⁇ 1) / 8”. Inch ”(for example, 3/8 inch), and“ (D o ⁇ 1) / 16 inch ”(for example, 3/16 inch) in the liquid side connection pipe 7 is set.
  • the refrigerant amount W 1 [kg] to be sealed in the refrigeration cycle apparatus using the refrigerant R32 having the rated refrigeration capacity Qc [kW] is W 1 [kg]
  • G R W 1 / W 0
  • the refrigerant amount W 1 sealed in a refrigeration cycle apparatus using the refrigerant R32 rated cooling capacity Qc [kW] [kg] can be expressed by the following equation.
  • the pipe outer diameter of the connection pipes 7 and 8 in the refrigeration cycle apparatus using R32 is set to the “(D o ⁇ 1) / 8 inch” in the gas side connection pipe 8, and the liquid side connection pipe 7
  • “(D o ⁇ 1) / 16 inch” it corresponds to the straight line (thin line) connecting the refrigerant amount ratios at the rated refrigeration capacity of less than 7.1 kW in FIG. 4, and the lower limit of the refrigerant amount ratio If the value is G RmB , from FIG.
  • the lower limit value of the refrigerant amount is set to By setting to “(0.011Qc + 0.60) W 0 [kg]”, the refrigerant can be converted from the refrigerant R410A to the refrigerant R32 without causing the performance of the refrigeration cycle apparatus to deteriorate.
  • the pipe outer diameters of the connection pipes 7 and 8 in the refrigeration cycle apparatus using the refrigerant R32 are divided according to the rated refrigeration capacity, the following is performed.
  • the rated refrigeration capacity is 7.1 kW or more
  • the pipe outer diameters of the connection pipes 7 and 8 are set to “(D o ⁇ 1) / 8 inch”, and the lower limit value of the refrigerant amount at this time is set to “(0.011Qc + 0 .60) W 0 [kg] ”.
  • the gas side connection pipe 8 is the “(D o ⁇ 1) / 8 inch”
  • the liquid side connection pipe 7 is the “(D o ⁇ 1) / 16 inch”.
  • FIG. 5 is based on the refrigeration cycle apparatus using the refrigerant R410A of the refrigeration cycle apparatus using the refrigerant R32 when the refrigerant amount of the refrigeration cycle apparatus using the refrigerant R32 and the refrigeration cycle apparatus using the refrigerant R410A are set to be the same.
  • the COP ratio is shown. Further, FIG. 5 also shows the connection pipe diameter used.
  • the COP ratio shown in FIG. 5 is that the lengths of the connecting pipes 7 and 8 are short connecting pipes (5 m for rated refrigeration capacities of 3.6 kW and 5.6 kW, rated refrigeration capacities of 7.1 kW and 12.5 kW). In the case of a thing, it is a thing when set to 7.5 m).
  • the refrigeration cycle using the refrigerant R32 is used.
  • the COP of the apparatus can be equal to or higher than the COP of the refrigeration cycle apparatus using the refrigerant R410A.
  • the pipe lengths of the connection pipes 7 and 8 can be set to be smaller than the refrigerant charging amount of the refrigeration cycle apparatus using the refrigerant R410A between the short pipe length and the maximum chargeless pipe length.
  • the refrigerant R410A having the same rated refrigeration capacity as the rated refrigeration capacity Qc [kW] of the refrigeration cycle apparatus using the refrigerant R32 at the lower limit values W 1mA and W 1mB of the refrigerant amount described above is used. It may be set to less than the refrigerant amount W 0 [kg] of the used refrigeration cycle apparatus.
  • the refrigeration cycle apparatus is the same as that shown in FIG. 1, and the parts not particularly mentioned have the same configuration as that shown in the first embodiment. ing.
  • the refrigeration cycle apparatus using the refrigerant R32 is used, and the connection pipe diameter is set to be smaller than that of the conventional refrigeration cycle apparatus using the refrigerant R410A. Therefore, the amount of refrigerant sealed in the refrigeration cycle can be reduced as compared with the conventional refrigeration cycle apparatus using the refrigerant R410A, and the amount of copper used as the material for the connection pipe can be reduced. Furthermore, by reducing the diameter of the connecting pipe, not only the amount of copper used can be reduced, but also the workability of the connecting pipe at the time of construction of the refrigeration air conditioner (refrigeration cycle apparatus) can be improved. Moreover, since R32 which is a low GWP refrigerant
  • the range of the refrigerant amount sealed in the refrigeration cycle apparatus using the refrigerant R32 is larger than the refrigerant quantity obtained based on the thick line or the thin line shown in FIG. 4, and the refrigerant enclosure in the conventional refrigeration cycle apparatus using the refrigerant R410A is performed. By reducing the amount, the refrigeration cycle apparatus having a high COP can be obtained.
  • a refrigeration cycle apparatus that can suppress a decrease in efficiency while using a refrigerant having a low global warming potential (GWP) and that can also reduce the pipe diameter of the connection pipe. An effect is obtained.
  • GWP global warming potential

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Compression-Type Refrigeration Machines With Reversible Cycles (AREA)
  • Other Air-Conditioning Systems (AREA)
  • Devices That Are Associated With Refrigeration Equipment (AREA)
  • Air Conditioning Control Device (AREA)

Abstract

The purpose of the present invention is to inhibit a reduction in efficiency and reduce the pipe diameter of connection pipes while a refrigerant having a low global warming potential (GWP) is used. A refrigerating cycle device is composed of a compressor (1), a heat source equipment-side heat exchanger (3), a first expansion device (4), a liquid-side connection pipe (7), a second expansion device (21), a usage-side heat exchange (22), and a gas-side connection pipe (8), the preceding being connected in the stated order. Also, the refrigerant used in the refrigerating cycle is R32, the outside diameter of the liquid-side connection pipe and the gas-side connection pipe is "D0/8 inches" (wherein "D0/8 inches" is the outside diameter of the connection pipe when refrigerant R410A is used), the range of D0 is "2 ≤ D0 ≤ 4" in the liquid connection pipe, and the range of D0 is "3 ≤ D0 ≤ 8" in the gas connection pipe.

Description

冷凍サイクル装置Refrigeration cycle equipment

 本発明は、冷凍サイクルを利用した空気調和機や冷凍機などの冷凍サイクル装置に関し、特に、冷凍サイクルに使用する冷媒としてR32(ジフルオロメタン)を使用したものに関する。 The present invention relates to a refrigeration cycle apparatus such as an air conditioner or a refrigerator using a refrigeration cycle, and particularly relates to one using R32 (difluoromethane) as a refrigerant used in the refrigeration cycle.

 現在、空気調和機や冷凍機などの冷凍空調機器では冷凍サイクル内に封入する冷媒として、冷媒R410Aを採用したものが増えている。冷媒R410Aは、冷凍空調機器の効率向上を図ることができ、それによる消費電力の低減により発電時の二酸化炭素発生量の削減を図ることができる。また、冷媒漏洩への対策等による冷媒排出の抑制も図ることで、地球温暖化防止に貢献している。 At present, in refrigeration and air-conditioning equipment such as air conditioners and refrigerators, an increasing number of refrigerants that employ refrigerant R410A as a refrigerant to be enclosed in the refrigeration cycle. The refrigerant R410A can improve the efficiency of the refrigerating and air-conditioning equipment, and can reduce the amount of carbon dioxide generated during power generation by reducing the power consumption. In addition, it contributes to the prevention of global warming by reducing refrigerant discharge by measures against refrigerant leakage.

 しかし、冷媒R410Aは、GWP(地球温暖化係数)の高い冷媒であるため、地球温暖化防止を更に進める観点から、冷媒R410AよりもGWPの低い冷媒を冷凍サイクル装置に使用することが望ましく、候補冷媒としては冷媒R32が考えられる。 
 この冷媒R32は、微燃性の特性を有しており、万が一の冷媒漏洩時における冷媒漏洩量の削減のため、冷凍サイクル内に封入する冷媒量を可能な限り削減することが好ましい。
However, since the refrigerant R410A is a refrigerant having a high GWP (global warming potential), it is desirable to use a refrigerant having a lower GWP than the refrigerant R410A in the refrigeration cycle apparatus from the viewpoint of further preventing global warming. A refrigerant R32 can be considered as the refrigerant.
The refrigerant R32 has a slightly flammable characteristic, and it is preferable to reduce the amount of refrigerant sealed in the refrigeration cycle as much as possible in order to reduce the amount of refrigerant leakage in the event of refrigerant leakage.

 また、冷媒R410Aから冷媒R32に転換することで室外機と室内機とを接続する接続配管(冷媒配管)の配管径を低減することができれば、封入する冷媒量を低減できるだけでなく、接続配管の材料である銅の使用量の削減も図れ、更に空気調和機などの施工時における接続配管の施工性向上を図ることも可能となる。 Moreover, if the pipe diameter of the connection pipe (refrigerant pipe) connecting the outdoor unit and the indoor unit can be reduced by converting the refrigerant R410A to the refrigerant R32, not only the amount of refrigerant to be sealed can be reduced, but also the connection pipe It is possible to reduce the amount of copper used as a material, and it is also possible to improve the workability of connection pipes during construction of air conditioners and the like.

 前記冷媒R32を使用した冷凍サイクル装置に関連する従来技術としては、特開2001-248941号公報(特許文献1)に記載のものや特開2002-89978号公報(特許文献2)に記載されたものがある。 
 上記特許文献1のものでは、冷媒R32を使用する冷凍サイクル装置において、液側接続配管とガス側接続配管の配管径を設定している。 
 また、上記特許文献2のものでは、冷媒R32を使用する冷凍サイクル装置において、冷凍サイクル内に封入する冷媒量を設定している。
Conventional techniques related to the refrigeration cycle apparatus using the refrigerant R32 are described in Japanese Patent Application Laid-Open No. 2001-248941 (Patent Document 1) and Japanese Patent Application Laid-Open No. 2002-89978 (Patent Document 2). There is something.
In the thing of the said patent document 1, in the refrigerating-cycle apparatus which uses refrigerant | coolant R32, the pipe diameter of the liquid side connection piping and the gas side connection piping is set.
Moreover, in the thing of the said patent document 2, in the refrigerating-cycle apparatus which uses refrigerant | coolant R32, the refrigerant | coolant amount enclosed in a refrigerating cycle is set.

特開2001-248941号公報JP 2001-248941 A 特開2002-89978号公報JP 2002-89978 A

 上記特許文献1に記載の従来技術は、HCFC冷媒である冷媒R22から冷媒R32への転換を考慮して、液側接続配管とガス側接続配管の配管径を設定しているが、冷媒R32を使用した場合の接続配管径の設定としては、必ずしも十分なものとなっていない。 In the prior art described in Patent Document 1, the diameters of the liquid side connection pipe and the gas side connection pipe are set in consideration of the conversion from the refrigerant R22, which is an HCFC refrigerant, to the refrigerant R32. When used, the connection pipe diameter is not always sufficient.

 即ち、現在多く使用されている冷媒R410Aから冷媒R32への転換で比較すると次のようになる。 
 冷媒R410Aを使用した冷凍サイクル装置における接続配管では、一般に次の配管径のものが使用されている。例えば、定格冷凍能力が4.5kW以上7.1kW未満の場合、液側接続配管の管外径は1/4インチ(6.35mm)、ガス側接続配管の管外径は1/2インチ(12.7mm)のものが使用され、定格冷凍能力が7.1kW以上14.0kW以下の場合には、液側接続配管の管外径は3/8インチ(9.53mm)、ガス側接続配管の管外径は5/8インチ(15.88mm)のものが使用されている。
That is, a comparison between the refrigerant R410A and refrigerant R32, which are currently widely used, is as follows.
In the connection piping in the refrigeration cycle apparatus using the refrigerant R410A, the following piping diameter is generally used. For example, when the rated refrigeration capacity is 4.5 kW or more and less than 7.1 kW, the outer diameter of the liquid side connecting pipe is 1/4 inch (6.35 mm), and the outer diameter of the gas side connecting pipe is 1/2 inch ( 12.7 mm) is used, and when the rated refrigeration capacity is 7.1 kW or more and 14.0 kW or less, the outer diameter of the liquid side connection pipe is 3/8 inch (9.53 mm), and the gas side connection pipe The outer diameter of the tube is 5/8 inch (15.88 mm).

 これに対して前記特許文献1のものでは、冷媒R32を使用した冷凍サイクル装置に使用する接続配管の管外径として、定格冷凍能力が4.5kW以上7.1kW以下の場合、液側接続配管の管外径は1/4インチ、ガス側接続配管の管外径は1/2インチのものを使用し、定格冷凍能力が7.1kW以上14.0kW以下の場合、液側接続配管の管外径は1/4インチ、ガス側接続配管の管外径は5/8インチのものを使用するようにしている。 On the other hand, in the thing of the said patent document 1, when rated refrigeration capacity is 4.5 kW or more and 7.1 kW or less as a pipe outer diameter of the connection piping used for the refrigerating cycle apparatus using refrigerant | coolant R32, liquid side connection piping If the pipe outside diameter is 1/4 inch and the gas side connecting pipe outside diameter is 1/2 inch and the rated refrigeration capacity is 7.1 kW to 14.0 kW, then the liquid side connecting pipe The outer diameter is 1/4 inch, and the gas-side connecting pipe has an outer diameter of 5/8 inch.

 上述した冷媒R410Aを使用した冷凍サイクル装置における接続配管径と、上記特許文献1に記載された冷媒R32を使用した接続配管径とを比較すると、定格冷凍能力が4.5kW以上7.1kW未満の場合、液側接続配管及びガス側接続配管径は冷媒R410Aで使用されているものと変わっていない。また、定格冷凍能力が7.1kWを超え14.0kW以下では、液側接続配管のみが細径化されている。このため、冷媒R410Aから冷媒R32への転換を考慮すると、接続配管径を細くすることによる銅管使用量の削減や施工性の向上はほとんど期待することはできないという課題がある。 When the connection pipe diameter in the refrigeration cycle apparatus using the refrigerant R410A described above is compared with the connection pipe diameter using the refrigerant R32 described in Patent Document 1, the rated refrigeration capacity is 4.5 kW or more and less than 7.1 kW. In this case, the diameters of the liquid side connection pipe and the gas side connection pipe are not different from those used in the refrigerant R410A. Further, when the rated refrigeration capacity exceeds 7.1 kW and is equal to or less than 14.0 kW, only the liquid side connection pipe is reduced in diameter. For this reason, when the conversion from the refrigerant R410A to the refrigerant R32 is taken into consideration, there is a problem that it is almost impossible to expect a reduction in the amount of copper pipe used and an improvement in workability by reducing the diameter of the connection pipe.

 上記特許文献2に記載の従来の技術のものでは、冷媒R32を冷凍サイクル装置に使用した際の冷凍サイクル内に封入する冷媒量を設定している。しかし、冷媒R32を使用した冷凍サイクル装置の接続配管径に関する記載も、また接続配管長に関する記載もなく、冷媒封入量の設定範囲も広いものとなっている。このため特許文献2に記載されている冷媒量封入量の設定範囲下限の量では、冷凍サイクル装置の施工時に冷媒を追加封入することなく、工場出荷時に封入した冷媒量のみでは、特に最大の接続配管長(チャージレス最大配管長)となる場合には、冷媒不足となる可能性があるという課題がある。 In the prior art described in Patent Document 2, the amount of refrigerant sealed in the refrigeration cycle when the refrigerant R32 is used in the refrigeration cycle apparatus is set. However, there is no description about the connection pipe diameter of the refrigeration cycle apparatus using the refrigerant R32, and there is no description about the connection pipe length, and the setting range of the refrigerant filling amount is wide. For this reason, in the amount of the setting range lower limit of the refrigerant amount enclosing amount described in Patent Document 2, the maximum connection is particularly achieved only by the amount of refrigerant encapsulated at the time of shipment from the factory, without additionally enclosing the refrigerant when constructing the refrigeration cycle apparatus. In the case of the pipe length (chargeless maximum pipe length), there is a problem that the refrigerant may be insufficient.

 本発明の目的は、地球温暖化係数(GWP)の低い冷媒を使用しつつ効率低下を抑制し、しかも接続配管の配管径も小さくすることのできる冷凍サイクル装置を得ることにある。 An object of the present invention is to obtain a refrigeration cycle apparatus that can suppress a decrease in efficiency while using a refrigerant having a low global warming potential (GWP) and that can also reduce the pipe diameter of a connection pipe.

 上記課題を解決するために、本発明は、圧縮機、熱源機側熱交換器、第1の膨張装置、液側接続配管、第2の膨張装置、利用側熱交換器、ガス側接続配管を順次接続して構成されている冷凍サイクル装置において、前記冷凍サイクルに使用する冷媒をR32とし、
 前記液側接続配管と、前記ガス側接続配管の管外径を、
   (D0-1)/8インチ
(ここで、「D0/8インチ」は冷媒R410Aを使用した場合の接続配管外径である)とし、且つ前記液接続配管では前記D0の範囲を「2≦D0≦4」とし、前記ガス接続配管では前記D0の範囲を「3≦D0≦8」としたことを特徴とする。
In order to solve the above problems, the present invention includes a compressor, a heat source unit side heat exchanger, a first expansion device, a liquid side connection pipe, a second expansion device, a use side heat exchanger, and a gas side connection pipe. In the refrigeration cycle apparatus configured to be sequentially connected, the refrigerant used in the refrigeration cycle is R32,
Pipe outer diameters of the liquid side connection pipe and the gas side connection pipe are:
(D 0 -1) / 8 inches (where "D 0/8 inches" is a connection pipe outer diameter in the case of using the refrigerant R410A) and, and the range of the D 0 in the liquid connection pipe " 2 ≦ D 0 ≦ 4 ”, and in the gas connection pipe, the range of D 0 is“ 3 ≦ D 0 ≦ 8 ”.

 ここで、定格冷凍能力が7.1kWから12.5kWまでの範囲では、前記液接続配管では前記D0を3(即ち配管径が1/4インチ)、前記ガス接続配管では前記D0を5(即ち配管径が1/2インチ)とし、定格冷凍能力が3.6kWから7.1kW未満の範囲では、前記液接続配管では前記D0を2.5(即ち配管径が3/16インチ)、前記ガス側接続配管では前記D0を4(即ち配管径が3/8インチ)とすることが好ましい。 Here, when the rated refrigeration capacity is in the range from 7.1 kW to 12.5 kW, the D 0 is 3 (that is, the pipe diameter is 1/4 inch) in the liquid connection pipe, and the D 0 is 5 in the gas connection pipe. (i.e., the pipe diameter of 1/2 inch) and, in a range of less than 7.1kW rated cooling capacity from 3.6kW, the D 0 2.5 (i.e. pipe diameter 3/16 inch) in the liquid connection pipe In the gas side connection pipe, the D 0 is preferably 4 (that is, the pipe diameter is 3/8 inch).

 本発明の他の特徴は、圧縮機、熱源機側熱交換器、第1の膨張装置、液側接続配管、第2の膨張装置、利用側熱交換器、ガス側接続配管を順次接続して構成されている冷凍サイクル装置において、前記冷凍サイクルに使用する冷媒をR32とし、前記液側接続配管と、前記ガス側接続配管の管外径を、
   D0/8インチ
とし、且つ前記液接続配管では前記D0の範囲を「1≦D0≦3」とし、前記ガス接続配管では前記D0の範囲を「2≦D0≦7」としたことにある。
Another feature of the present invention is that the compressor, the heat source unit side heat exchanger, the first expansion device, the liquid side connection piping, the second expansion device, the use side heat exchanger, and the gas side connection piping are sequentially connected. In the refrigeration cycle apparatus configured, the refrigerant used in the refrigeration cycle is R32, and the liquid side connection pipe and the pipe outer diameter of the gas side connection pipe are:
D 0/8 inches, and in the liquid connection pipe, the range of D 0 is “1 ≦ D 0 ≦ 3”, and in the gas connection pipe, the range of D 0 is “2 ≦ D 0 ≦ 7”. There is.

 ここで、定格冷凍能力が7.1kWから12.5kWまでの範囲では、前記液接続配管では前記D0を2(即ち配管径が1/4インチ)、前記ガス接続配管では前記D0を4(即ち配管径が1/2インチ)とし、定格冷凍能力が3.6kWから7.1kW未満の範囲では、前記液接続配管では前記D0を1.5(即ち配管径が3/16インチ)、前記ガス側接続配管では前記D0を3(即ち配管径が3/8インチ)とすることが好ましい。 Here, in the range from the rated cooling capacity is 7.1kW up to 12.5 kW, the liquid connection piping the D 0 2 (i.e. pipe diameter is 1/4 inches), the D 0 is the gas connection pipe 4 (i.e., the pipe diameter of 1/2 inch) and, in a range of less than 7.1kW rated cooling capacity from 3.6kW, the liquid connecting the D 0 1.5 (i.e. pipe diameter 3/16 inch) in the pipe In the gas side connection pipe, the D 0 is preferably 3 (that is, the pipe diameter is 3/8 inch).

 また、上記の冷凍サイクル装置において、冷凍サイクル装置への冷媒R32の封入量を、冷媒としてR410Aを使用し且つ定格冷凍能力が同一で同一仕様の冷凍サイクル装置に封入している冷媒R410Aの封入量よりも少ない封入量に設定すると良い。 Further, in the above refrigeration cycle apparatus, the amount of refrigerant R32 enclosed in the refrigeration cycle apparatus is equal to the amount of refrigerant R410A enclosed in the same specification refrigeration cycle apparatus using R410A as the refrigerant and having the same rated refrigeration capacity. It is better to set a smaller amount.

 更に、冷凍サイクル装置への冷媒R32の封入量をW1[kg]、前記冷凍サイクル装置の定格冷凍能力をQc[kW]、冷媒R410Aを使用した同一の定格冷凍能力Qc[kW]の冷凍サイクル装置における冷媒封入量をW0[kg]としたとき、前記冷媒R32を使用した前記冷凍サイクル装置への前記冷媒封入量W1を、
 Qc≧7.1kWでは、
   (0.011Qc+0.60)W0≦W1<W0
 Qc<7.1kWでは、
   (0.030Qc+0.71)W0≦W1<W0
の範囲に設定することが好ましい。
Furthermore, the amount of refrigerant R32 enclosed in the refrigeration cycle apparatus is W 1 [kg], the refrigeration cycle apparatus has a rated refrigeration capacity of Qc [kW], and the refrigeration cycle having the same rated refrigeration capacity Qc [kW] using the refrigerant R410A. When the refrigerant filling amount in the apparatus is W 0 [kg], the refrigerant filling amount W 1 to the refrigeration cycle apparatus using the refrigerant R32 is
For Qc ≧ 7.1 kW,
(0.011Qc + 0.60) W 0 ≦ W 1 <W 0
For Qc <7.1 kW,
(0.030Qc + 0.71) W 0 ≦ W 1 <W 0
It is preferable to set in the range.

 本発明によれば、地球温暖化係数(GWP)の低い冷媒を使用しつつ効率低下を抑制し、しかも接続配管の配管径も小さくすることのできる冷凍サイクル装置を得ることができる。 According to the present invention, it is possible to obtain a refrigeration cycle apparatus that can suppress a decrease in efficiency while using a refrigerant having a low global warming potential (GWP) and that can also reduce the pipe diameter of the connection pipe.

本発明の冷凍サイクル装置の実施例1を説明するサイクル系統図。The cycle system diagram explaining Example 1 of the refrigerating-cycle apparatus of this invention. 同等のCOPとなる冷媒R410AとR32を使用した冷凍サイクル装置(定格冷凍能力7.1kW、12.5kW)における接続配管径と、冷媒量比を説明する図。The figure explaining the connection pipe diameter and refrigerant | coolant amount ratio in the refrigerating-cycle apparatus (Rated refrigerating capacity 7.1kW, 12.5kW) using refrigerant | coolant R410A and R32 used as equivalent COP. 同等のCOPとなる冷媒R410AとR32を使用した冷凍サイクル装置(定格冷凍能力3.6kW、5.6kW)における接続配管径と、冷媒量比を説明する図。The figure explaining the connection piping diameter and refrigerant | coolant amount ratio in the refrigerating-cycle apparatus (Rated refrigerating capacity 3.6kW, 5.6kW) using refrigerant | coolant R410A and R32 used as equivalent COP. 冷媒R32を使用した冷凍サイクル装置において、定格冷凍能力に対するR410A基準の冷媒量比(COPが同等となる冷媒量比)を示す線図。The refrigeration cycle apparatus using refrigerant | coolant R32 WHEREIN: The diagram which shows refrigerant | coolant amount ratio (refrigerant | quantitative amount ratio in which COP is equivalent) of R410A with respect to rated refrigeration capacity. 冷媒R410AとR32を使用した冷凍サイクル装置において、冷媒量を同等とした場合におけるR410A基準のCOP比を説明する図で、接続配管径も併せて表示している図。In the refrigerating cycle device using refrigerant | coolant R410A and R32, it is a figure explaining the C410 ratio of R410A reference | standard when the refrigerant | coolant amount is made equivalent, The figure which also displays the connection piping diameter.

 以下本発明の冷凍サイクル装置の具体的実施例を図面に基づいて説明する。 Hereinafter, specific embodiments of the refrigeration cycle apparatus of the present invention will be described with reference to the drawings.

 本発明の冷凍サイクル装置の実施例1を図1~図3により説明する。図1は本発明の冷凍サイクル装置の実施例1を説明するサイクル系統図、図2は同様のCOPとなる冷媒R410AとR32を使用した冷凍サイクル装置(定格冷凍能力7.1kW、12.5kW)における接続配管径と、冷媒量比を説明する図、図3は同様のCOPとなる冷媒R410AとR32を使用した冷凍サイクル装置(定格冷凍能力3.6kW、5.6kW)における接続配管径と、冷媒量比を説明する図である。 Embodiment 1 of the refrigeration cycle apparatus of the present invention will be described with reference to FIGS. FIG. 1 is a cycle system diagram illustrating Example 1 of the refrigeration cycle apparatus of the present invention, and FIG. 2 is a refrigeration cycle apparatus using refrigerants R410A and R32 serving as the same COP (rated refrigeration capacity 7.1 kW, 12.5 kW). FIG. 3 is a diagram for explaining the connection pipe diameter and the refrigerant amount ratio in FIG. 3. FIG. 3 shows the connection pipe diameter in the refrigeration cycle apparatus (rated refrigeration capacity 3.6 kW, 5.6 kW) using the refrigerants R410A and R32, which are similar COPs. It is a figure explaining refrigerant | coolant amount ratio.

 図1は冷凍サイクル装置としての空気調和機を示しており、室外機40と室内機20とが液側接続配管7とガス側接続配管8により接続されている。前記室外機40において、1は圧縮機(密閉式圧縮機)、2は四方弁、3は熱源機側熱交換器、4は第1の膨張装置、6は液側の阻止弁、9はガス側の阻止弁、10はアキュームレータである。また、前記室内機20において、21は第2の膨張装置、22は利用側熱交換器である。前記圧縮機1、熱源機側熱交換器3、第1の膨張装置4、液側接続配管7、第2の膨張装置21、利用側熱交換器22、ガス側接続配管8などは順次接続配管(冷媒配管)で接続されて冷凍サイクル装置(本実施例では空気調和機)が構成されている。 FIG. 1 shows an air conditioner as a refrigeration cycle apparatus, in which an outdoor unit 40 and an indoor unit 20 are connected by a liquid side connection pipe 7 and a gas side connection pipe 8. In the outdoor unit 40, 1 is a compressor (sealed compressor), 2 is a four-way valve, 3 is a heat source side heat exchanger, 4 is a first expansion device, 6 is a liquid side blocking valve, and 9 is a gas. The side stop valve 10 is an accumulator. In the indoor unit 20, 21 is a second expansion device, and 22 is a use side heat exchanger. The compressor 1, the heat source device side heat exchanger 3, the first expansion device 4, the liquid side connection piping 7, the second expansion device 21, the use side heat exchanger 22, the gas side connection piping 8, etc. are sequentially connected piping. (Refrigerant piping) is connected and the refrigerating cycle apparatus (an air conditioner in a present Example) is comprised.

 冷房運転の場合、前記圧縮機1で圧縮されて高温高圧となったガス冷媒は、冷凍機油と共に前記圧縮機1から吐出され、このガス冷媒は前記四方弁2を経て、前記熱源機側熱交換器3へと流入し、ここで熱交換して凝縮液化する。凝縮液化した冷媒は全開とされた第1の膨張装置4を通り、その後阻止弁6、液側接続配管7を通過して、前記室内機20へ送られる。前記室内機20送られた液冷媒は、第2の膨張装置21へ流入し、ここで減圧されて低圧の二相状態となり、利用側熱交換器22で空気等の利用側媒体と熱交換して蒸発・ガス化する。その後、ガス冷媒はガス側接続配管8、阻止弁9を通過し、四方弁2を経由して再び前記圧縮機1へと戻る。余剰冷媒はアキュムレータ10に貯留されることで、冷凍サイクルの運転圧力、温度が正常な状態に保たれる。 In the case of cooling operation, the gas refrigerant compressed by the compressor 1 to become high temperature and pressure is discharged from the compressor 1 together with refrigeration oil, and the gas refrigerant passes through the four-way valve 2 to exchange heat with the heat source unit. It flows into the vessel 3, where it exchanges heat and condensates. The condensed and liquefied refrigerant passes through the fully expanded first expansion device 4, and then passes through the blocking valve 6 and the liquid side connection pipe 7, and is sent to the indoor unit 20. The liquid refrigerant sent to the indoor unit 20 flows into the second expansion device 21, where it is decompressed to become a low-pressure two-phase state, and exchanges heat with the utilization side medium such as air in the utilization side heat exchanger 22. Evaporate and gasify. Thereafter, the gas refrigerant passes through the gas side connection pipe 8 and the blocking valve 9 and returns to the compressor 1 again via the four-way valve 2. The surplus refrigerant is stored in the accumulator 10 so that the operating pressure and temperature of the refrigeration cycle are maintained in a normal state.

 暖房運転の場合、圧縮機1で圧縮されて高温高圧となったガス冷媒は、冷凍機油と共に圧縮機1から吐出される。このガス冷媒は、四方弁2により阻止弁9側に流れ、ガス側接続配管8を経て前記室内機20の利用側熱交換器22へ流入する。ここで前記ガス冷媒は空気等の利用側媒体と熱交換して凝縮液化する。凝縮液化した冷媒は、液側接続配管7、阻止弁6を経て、第1の膨張装置4で減圧され、前記熱源機側熱交換器3で空気や水等の熱源媒体と熱交換して蒸発・ガス化する。蒸発・ガス化した冷媒は、四方弁2を経て再び圧縮機1へと戻る。 In the heating operation, the gas refrigerant compressed into the high temperature and high pressure by the compressor 1 is discharged from the compressor 1 together with the refrigerating machine oil. The gas refrigerant flows to the blocking valve 9 side by the four-way valve 2 and flows into the use side heat exchanger 22 of the indoor unit 20 through the gas side connection pipe 8. Here, the gas refrigerant is condensed and liquefied by exchanging heat with a use side medium such as air. The condensed and liquefied refrigerant is depressurized by the first expansion device 4 through the liquid side connection pipe 7 and the blocking valve 6, and is evaporated by exchanging heat with a heat source medium such as air or water in the heat source unit side heat exchanger 3.・ Gasify. The evaporated and gasified refrigerant returns to the compressor 1 again through the four-way valve 2.

 本実施例の冷凍サイクル装置は冷媒としてR32を使用しており、前記液側接続配管7及びガス側接続配管8の管外径を、冷媒R410Aを使用した同一定格冷凍能力の冷凍サイクル装置よりも1ランク細く設定している。 
 以下、前記接続配管7,8の管外径の設定について詳しく説明する。なお、本実施例では冷媒量がより多く必要となる冷房運転の場合について説明する。
The refrigeration cycle apparatus of the present embodiment uses R32 as a refrigerant, and the outer diameters of the liquid side connection pipe 7 and the gas side connection pipe 8 are made larger than those of the refrigeration cycle apparatus having the same rated refrigeration capacity using the refrigerant R410A. One rank is set thin.
Hereinafter, the setting of the pipe outer diameter of the connection pipes 7 and 8 will be described in detail. In the present embodiment, the case of cooling operation in which a larger amount of refrigerant is required will be described.

 冷媒量は、例えば冷凍サイクルの内容積(圧縮機1、熱源機側熱交換器3、液側接続配管7、利用側熱交換器22、ガス側接続配管8、アキュムレータ10などの内容積)と冷媒の密度に応じて決めることができる。また、前記圧縮機1に封入されている冷凍機油に溶解する分の冷媒量や、前記第1の膨張装置4と液側の前記阻止弁6との間にレシーバが設置されるタイプの冷凍サイクル装置ではレシーバの内容積も考慮して冷媒量を決めるとなお好ましい。 The refrigerant amount is, for example, the internal volume of the refrigeration cycle (the internal volume of the compressor 1, the heat source machine side heat exchanger 3, the liquid side connection pipe 7, the use side heat exchanger 22, the gas side connection pipe 8, the accumulator 10, etc.) It can be determined according to the density of the refrigerant. In addition, the amount of refrigerant dissolved in the refrigerating machine oil sealed in the compressor 1 and a refrigerating cycle in which a receiver is installed between the first expansion device 4 and the liquid side blocking valve 6. In the apparatus, it is more preferable to determine the refrigerant amount in consideration of the internal volume of the receiver.

 同等のCOP(=冷凍能力/消費電力)となる冷媒R410AとR32を使用した冷凍サイクル装置で、定格冷凍能力が7.1kWと12.5kWにおける接続配管径と、冷媒量比を図2により説明する。即ち、図2は、冷媒R410Aを使用した冷凍サイクル装置のCOPと同等にするために最低限必要となる、冷媒R32を使用した冷凍サイクル装置の冷媒量を、冷媒R410Aを使用した冷凍サイクル装置を基準とした冷媒量比で示している図である。前記接続配管7,8の長さは、工場出荷時に封入した冷媒量のみで対応可能な最大の接続配管長(チャージレス最大配管長)とし、定格冷凍能力が7.1kWと12.5kWでは30mである。 FIG. 2 illustrates the connection pipe diameter and the refrigerant amount ratio when the rated refrigeration capacities are 7.1 kW and 12.5 kW in the refrigeration cycle apparatus using the refrigerants R410A and R32 having the same COP (= refrigeration capacity / power consumption). To do. That is, FIG. 2 shows the refrigerant amount of the refrigeration cycle apparatus using the refrigerant R32, which is the minimum required to be equivalent to the COP of the refrigeration cycle apparatus using the refrigerant R410A, and the refrigeration cycle apparatus using the refrigerant R410A. It is the figure shown with the refrigerant | coolant amount ratio used as the reference | standard. The length of the connecting pipes 7 and 8 is the maximum connecting pipe length (chargeless maximum pipe length) that can be handled only by the amount of refrigerant sealed at the time of shipment from the factory, and is 30 m when the rated refrigeration capacity is 7.1 kW and 12.5 kW. It is.

 なお、前記接続配管7,8がチャージレス最大配管長以上の場合は、施工時にチャージレス最大配管長を超過した配管の長さに応じて、所定の冷媒量を追加することで対応可能である。 In addition, when the connection pipes 7 and 8 are longer than the chargeless maximum pipe length, it can be dealt with by adding a predetermined refrigerant amount according to the length of the pipe that exceeds the chargeless maximum pipe length at the time of construction. .

 以下説明するCOP比及び冷媒量比の検討には、冷凍サイクルの運転状態を模擬するサイクルシミュレータ(例えば、第34回空気調和・冷凍連合講演会論文集(2000年4月17~19日)の13~16頁、2005年度日本冷凍空調学会年次大会講演論文集(2005年10月23~27日)のB204-1~4を参照)による計算値を使用した。 To examine the COP ratio and refrigerant amount ratio described below, a cycle simulator that simulates the operating state of the refrigeration cycle (for example, the 34th Air Conditioning and Refrigeration Union Lecture Proceedings (April 17-19, 2000) The calculated values from pages 13 to 16 (see B204-1 to 4 of 2005 Annual Conference of the Japan Society of Refrigerating and Air Conditioning Engineers Annual Conference (October 23 to 27, 2005)) were used.

 図2に示すように、本実施例では、冷媒R32を使用した冷凍サイクル装置の接続配管7,8の管外径は、冷媒R410Aを使用した冷凍サイクル装置の接続配管7,8の管外径を「D0/8インチ」としたとき(但し、本実施例では、前記D0の範囲を、液接続配管7では「2≦D0≦4」とし、ガス接続配管8では「3≦D0≦8」とする)、これよりも1ランク細い管外径、即ち「(D0-1)/8インチ」に設定している。 
 即ち、前記接続配管7,8の管外径は、冷媒R410Aを使用した冷凍サイクル装置のものでは、一般に、ガス側接続配管8は5/8インチ(15.88mm)、液側接続配管7は3/8インチ(9.53mm)のものが使用されているので、図2の説明でも前述した管外径のものを使用しているものとする。これに対して、本実施例の冷媒R32を使用した冷凍サイクル装置では、接続配管7,8の管外径はガス側接続配管8及び液側接続配管7共に、1ランク細い管外径のものを使用しているので、ガス側接続配管8では4/8インチ(=1/2インチ:12.7mm)であり、液側接続配管7では2/8インチ(=1/4インチ:6.35mm)のものを使用している。
As shown in FIG. 2, in this embodiment, the pipe outer diameters of the connection pipes 7 and 8 of the refrigeration cycle apparatus using the refrigerant R32 are the pipe outer diameters of the connection pipes 7 and 8 of the refrigeration cycle apparatus using the refrigerant R410A. Is “D 0/8 inch” (however, in this embodiment, the range of D 0 is “2 ≦ D 0 ≦ 4” in the liquid connection pipe 7 and “3 ≦ D in the gas connection pipe 8”. 0 ≦ 8 ”), the outer diameter of the pipe is one rank smaller than this, ie,“ (D 0 −1) / 8 inch ”.
That is, the pipe outer diameters of the connection pipes 7 and 8 are generally 5/8 inch (15.88 mm) for the gas side connection pipe 8 and the liquid side connection pipe 7 for the refrigeration cycle apparatus using the refrigerant R410A. Since a 3/8 inch (9.53 mm) one is used, it is assumed that the above-mentioned tube outer diameter is also used in the description of FIG. On the other hand, in the refrigeration cycle apparatus using the refrigerant R32 of this embodiment, the pipe outer diameters of the connection pipes 7 and 8 are one rank narrower pipe outer diameter for both the gas side connection pipe 8 and the liquid side connection pipe 7. Therefore, the gas side connection pipe 8 is 4/8 inch (= 1/2 inch: 12.7 mm), and the liquid side connection pipe 7 is 2/8 inch (= 1/4 inch: 6.2. 35mm) is used.

 この図2からわかるように、冷媒R32を使用した冷凍サイクル装置においては、接続配管7,8の管外径を、冷媒R410Aを使用した冷凍サイクル装置での接続配管7,8の管外径よりも1ランク細く設定することで、以下の効果が得られる。 
 即ち、図2の表は、COPが冷媒R410Aを使用した冷凍サイクル装置のCOPと同等であるから、冷凍空調機器の性能を低下させることなく、銅の使用量の削減や施工時の接続配管の施工性を向上した冷凍サイクル装置を得ることができる。また、冷凍空調機器使用時の電力量は、R410Aを使用した場合と同等であるから、発電に伴う電力使用時の二酸化炭素の排出量を増加させることなく、低GWP(地球温暖化係数)の冷媒R32を使用しているため、地球温暖化防止に効果のある冷凍サイクル装置を得ることができる。更に、接続配管7,8の管外径を細くできることにより、前記接続配管の材料である銅の使用量の削減を図ることができ、しかも冷凍空調機器施工時における接続配管の施工性の向上も図ることのできる冷凍サイクル装置を得ることができる。
As can be seen from FIG. 2, in the refrigeration cycle apparatus using the refrigerant R32, the pipe outer diameters of the connection pipes 7 and 8 are larger than the pipe outer diameters of the connection pipes 7 and 8 in the refrigeration cycle apparatus using the refrigerant R410A. In addition, the following effects can be obtained by setting the 1 rank narrower.
That is, the table in FIG. 2 shows that the COP is equivalent to the COP of the refrigeration cycle apparatus using the refrigerant R410A, so that the amount of copper used can be reduced and the connection piping at the time of construction can be reduced without degrading the performance of the refrigeration air conditioning equipment. A refrigeration cycle apparatus with improved workability can be obtained. In addition, the amount of power when using refrigeration and air-conditioning equipment is the same as when using R410A, so low GWP (global warming potential) is achieved without increasing the amount of carbon dioxide emissions when using power accompanying power generation. Since the refrigerant R32 is used, a refrigeration cycle apparatus effective for preventing global warming can be obtained. Furthermore, by reducing the pipe outer diameter of the connection pipes 7 and 8, it is possible to reduce the amount of copper used as the material for the connection pipes, and also to improve the workability of the connection pipes during construction of refrigeration and air conditioning equipment. A refrigeration cycle apparatus that can be realized can be obtained.

 なお、図2の例では、定格冷凍能力が7.1kWと12.5kWについて説明しているが、これらの間の定格冷凍能力の冷凍サイクル装置についても、ガス側接続配管径及び液側接続配管径は図2に示すものと同様である。 In the example of FIG. 2, the rated refrigeration capacities of 7.1 kW and 12.5 kW are described. However, the refrigeration cycle apparatus having the rated refrigeration capacities between them also has a gas side connection pipe diameter and a liquid side connection pipe. The diameter is the same as that shown in FIG.

 図3は、定格冷凍能力が3.6kWと5.6kWの冷凍サイクル装置において、冷媒R410Aを使用した冷凍サイクル装置のCOPと同等にするために最低限必要となる、冷媒R32を使用した冷凍サイクル装置の冷媒量を、冷媒R410Aを使用した冷凍サイクル装置を基準とした冷媒量比で示している図である。接続配管7,8の長さは、工場出荷時に封入した冷媒量のみで対応可能な最大の接続配管長(チャージレス最大配管長)である20mとしている。 FIG. 3 shows a refrigeration cycle using the refrigerant R32, which is at least required to be equivalent to the COP of the refrigeration cycle apparatus using the refrigerant R410A in the refrigeration cycle apparatuses having the rated refrigeration capacities of 3.6 kW and 5.6 kW. It is a figure which shows the refrigerant | coolant amount of an apparatus by the refrigerant | coolant amount ratio on the basis of the refrigerating-cycle apparatus which uses refrigerant | coolant R410A. The length of the connection pipes 7 and 8 is 20 m which is the maximum connection pipe length (chargeless maximum pipe length) that can be handled only by the amount of refrigerant sealed at the time of shipment from the factory.

 図3に示すように、本実施例では、冷媒R32を使用した冷凍サイクル装置の接続配管7,8の管外径は、冷媒R410Aを使用した冷凍サイクル装置の接続配管7,8の管外径を「D0/8インチ」としたとき、これよりも1ランク細い管外径、即ち「(D0-1)/8インチ」または「(D0-1)/16インチ」に設定している。 
 即ち、前記接続配管7,8の管外径は、冷媒R410Aを使用した冷凍サイクル装置のものでは、一般に、ガス側接続配管8は4/8(=1/2)インチ(12.7mm)、液側接続配管7は2/8(=1/4)インチ(6.35mm)のものが使用されているので、図3の説明でもこれらの管外径のものを使用しているものとする。これに対して、本実施例の冷媒R32を使用した冷凍サイクル装置では、接続配管7,8の管外径はガス側接続配管8では、1ランク細い管外径のもの((D0-1)/8インチ)を使用しているので、ガス側接続配管8では3/8インチ(9.53mm)のものを使用している。
As shown in FIG. 3, in this embodiment, the pipe outer diameters of the connection pipes 7 and 8 of the refrigeration cycle apparatus using the refrigerant R32 are the pipe outer diameters of the connection pipes 7 and 8 of the refrigeration cycle apparatus using the refrigerant R410A. the when the "D 0/8 inches", 1 rank thin tube outer diameter than this, that is, set to "(D 0 -1) / 8 inches" or "(D 0 -1) / 16 inches" Yes.
That is, the pipe outer diameters of the connection pipes 7 and 8 are generally 4/8 (= 1/2) inch (12.7 mm) for the gas side connection pipe 8 in the refrigeration cycle apparatus using the refrigerant R410A. Since the liquid side connection pipe 7 of 2/8 (= 1/4) inch (6.35 mm) is used, it is assumed that those of the outside diameters of these pipes are also used in the description of FIG. . On the other hand, in the refrigeration cycle apparatus using the refrigerant R32 of the present embodiment, the connection pipes 7 and 8 have a pipe outer diameter that is one rank narrower in the gas side connection pipe 8 ((D 0 −1 ) / 8 inch), the gas side connecting pipe 8 is 3/8 inch (9.53 mm).

 液側接続配管7の場合、冷媒R410Aでの液側接続配管7の管外径は2/8(=1/4)インチ(6.35mm)であり、前記「(D0-1)/8インチ」を適用すると、冷媒R32を使用した冷凍サイクル装置では、管外径が1/8インチ(3.18mm)となる。しかし、1/8インチという細い接続配管を使用すると、冷媒流量によっては液側接続配管7内での圧力損失が過大となり、前記第2の膨張装置21での冷媒側流路抵抗の調整範囲を超えることがあり、前記圧縮機1の吸入圧力が該圧縮機1の運転範囲外まで低下し、冷凍サイクル装置の信頼性を低下させる可能性がある。 In the case of the liquid side connection pipe 7, the outer diameter of the liquid side connection pipe 7 with the refrigerant R410A is 2/8 (= 1/4) inch (6.35 mm), and the “(D 0 −1) / 8” is described above. When “inch” is applied, the outer diameter of the pipe is 1/8 inch (3.18 mm) in the refrigeration cycle apparatus using the refrigerant R32. However, if a thin connection pipe of 1/8 inch is used, the pressure loss in the liquid side connection pipe 7 becomes excessive depending on the refrigerant flow rate, and the adjustment range of the refrigerant side flow path resistance in the second expansion device 21 is increased. In some cases, the suction pressure of the compressor 1 falls outside the operating range of the compressor 1, which may reduce the reliability of the refrigeration cycle apparatus.

 このため、本実施例では、液側接続配管7のより好ましい配管径(管外径)として図3に示したものを使用している。即ち、冷媒R410Aを使用した冷凍サイクル装置の液側接続配管7の管外径は1/4(=4/16)インチであるので、前記「(D0-1)/16インチ」を適用して1ランク細い管外径である3/16インチ(=1.5/8)(4.76mm)のものを使用している。 For this reason, in the present Example, what was shown in FIG. 3 as a more preferable piping diameter (pipe outer diameter) of the liquid side connection piping 7 is used. That is, since the pipe outer diameter of the liquid side connection pipe 7 of the refrigeration cycle apparatus using the refrigerant R410A is 1/4 (= 4/16) inch, the “(D 0 −1) / 16 inch” is applied. 3/16 inch (= 1.5 / 8) (4.76 mm), which is a pipe outer diameter that is one rank thinner.

 なお、前記液側接続配管7の径を前記「(D0-1)/8」で表現すれば、前記D0は2.5となる(この場合前記液側接続配管7の外径は1.5/8(3/16)インチとなる)。 If the diameter of the liquid side connection pipe 7 is expressed by “(D 0 −1) / 8”, the D 0 is 2.5 (in this case, the outer diameter of the liquid side connection pipe 7 is 1). .5 / 8 (3/16) inch).

 また、上述した例では、前記接続配管7,8の径を、冷媒R410Aを使用した冷凍サイクル装置の接続配管7,8の管外径を「D0/8インチ」とし、これを基準として本実施例の冷媒R32を使用した冷凍サイクル装置における接続配管径を、前記「(D0-1)/8インチ」または「(D0-1)/16インチ」で表現している。ここで、冷媒R410Aを使用した冷凍サイクル装置の接続配管7,8の管外径を基準としないで、冷媒R32を使用した冷凍サイクル装置における接続配管径を表現すれば、「D0/8」として表現できる(但し、この場合は、前記D0の範囲を、前記液接続配管7では「1≦D0≦3」とし、前記ガス接続配管8では「2≦D0≦7」にする)。 Further, according to the example described above, the diameter of the connection pipe 7 and 8, the outer diameter of the connection pipe 7 and 8 of the refrigeration cycle apparatus using the refrigerant R410A is "D 0/8 inches", this as a reference The connection pipe diameter in the refrigeration cycle apparatus using the refrigerant R32 of the example is expressed by the above “(D 0 −1) / 8 inch” or “(D 0 −1) / 16 inch”. Here, if the connection pipe diameter in the refrigeration cycle apparatus using the refrigerant R32 is expressed without using the pipe outer diameters of the connection pipes 7 and 8 of the refrigeration cycle apparatus using the refrigerant R410A as “D 0/8 ”, (However, in this case, the range of D 0 is “1 ≦ D 0 ≦ 3” in the liquid connection pipe 7 and “2 ≦ D 0 ≦ 7” in the gas connection pipe 8). .

 この場合、図2に示す定格冷凍能力が7.1kWから12.5kWまでの範囲では、前記液接続配管7では前記D0は2(即ち配管径が1/4インチ)、前記ガス接続配管8では前記D0は4(即ち配管径が1/2インチ)となる。また、図3に示す定格冷凍能力が3.6kWから7.1kW未満の範囲では、前記液接続配管7では前記D0は1.5(「D0/16」として表現すれば前記D0は3)(即ち配管径が3/16インチ)、前記ガス側接続配管8では前記D0は3(即ち配管径が3/8インチ)となる。 In this case, in the range of the rated refrigeration capacity shown in FIG. 2 from 7.1 kW to 12.5 kW, in the liquid connection pipe 7, the D 0 is 2 (that is, the pipe diameter is 1/4 inch), and the gas connection pipe 8 Then, the D 0 is 4 (that is, the pipe diameter is 1/2 inch). Further, in the range of less than 7.1kW from the rated cooling capacity is 3.6kW shown in FIG. 3, the D 0 be expressed as the D 0 in the liquid connection pipe 7 is 1.5 ( "D 0/16" is 3) (that is, the pipe diameter is 3/16 inch), and in the gas side connection pipe 8, the D 0 is 3 (that is, the pipe diameter is 3/8 inch).

 このように、本実施例では、冷媒R32を使用した冷凍サイクル装置の液側接続配管7として、1/8インチよりも太い3/16インチを使用しているので、冷凍サイクル装置の信頼性を低下させず、また冷凍空調機器の性能も低下させずに、前記接続配管7,8の管外径を細くすることができる。これにより、銅管の使用量の削減や施工時の接続配管の施工性を向上でき、また低GWPの冷媒R32を使用しているので、地球温暖化防止に効果のある冷凍サイクル装置を得ることができる。 As described above, in this embodiment, 3/16 inch thicker than 1/8 inch is used as the liquid side connection pipe 7 of the refrigeration cycle device using the refrigerant R32, so that the reliability of the refrigeration cycle device is improved. The outer diameters of the connecting pipes 7 and 8 can be reduced without lowering the performance of the refrigerating and air-conditioning equipment. As a result, the amount of copper pipe used can be reduced and the workability of connecting pipes during construction can be improved, and since a low-GWP refrigerant R32 is used, a refrigeration cycle apparatus effective for preventing global warming can be obtained. Can do.

 なお、図3の例では、定格冷凍能力が3.6kWと5.6kWについて説明しているが、これらの間の定格冷凍能力の冷凍サイクル装置、及び5.6kWを超え7.1kW未満の定格冷凍能力の冷凍サイクル装置についても、ガス側接続配管径及び液側接続配管径は図3に示すものと同様である。 In the example of FIG. 3, the rated refrigeration capacities of 3.6 kW and 5.6 kW are described, but a refrigeration cycle apparatus having a rated refrigeration capacity between these, and a rating of more than 5.6 kW and less than 7.1 kW Also in the refrigeration cycle apparatus having the refrigeration capacity, the gas side connection pipe diameter and the liquid side connection pipe diameter are the same as those shown in FIG.

 以上述べたように、定格冷凍能力が3.6kWを超え7.1kW未満の冷媒R32を使用した冷凍サイクル装置では、ガス側接続配管8の管外径としては3/8インチを採用し、液側接続配管7の管外径としては、3/16インチを採用することが好ましい。 As described above, in the refrigeration cycle apparatus using the refrigerant R32 having a rated refrigeration capacity of more than 3.6 kW and less than 7.1 kW, the outer diameter of the gas-side connecting pipe 8 is 3/8 inch. As the pipe outer diameter of the side connection pipe 7, it is preferable to adopt 3/16 inch.

 本発明の冷凍サイクル装置の実施例2を図4、図5により説明する。図4は冷媒R32を使用した冷凍サイクル装置において、定格冷凍能力に対するR410A基準の冷媒量比(COPが同等となる冷媒量比)を示す線図、図5は冷媒R410AとR32を使用した冷凍サイクル装置において、冷媒量を同等とした場合におけるR410A基準のCOP比を説明する図で、接続配管径も併せて表示している図である。 Embodiment 2 of the refrigeration cycle apparatus of the present invention will be described with reference to FIGS. FIG. 4 is a diagram illustrating a refrigerant amount ratio (refrigerant amount ratio at which COP is equivalent) with respect to the rated refrigeration capacity in a refrigeration cycle apparatus using refrigerant R32, and FIG. 5 is a refrigeration cycle using refrigerants R410A and R32. In the apparatus, it is a figure explaining the COP ratio of R410A standard when the amount of refrigerant | coolants is made equivalent, and is a figure which also displays the connection piping diameter.

 上記実施例1では、冷媒R32を使用した冷凍サイクル装置の接続配管7,8の管外径を、冷媒R410Aを使用した冷凍サイクル装置のそれよりも1ランク細い接続配管を使用しているが、図4により、前記冷媒R32を使用した冷凍サイクル装置に封入する冷媒量(上限値と下限値)について説明する。 In Example 1 above, the connecting pipes 7 and 8 of the refrigeration cycle apparatus using the refrigerant R32 have a pipe outer diameter that is one rank lower than that of the refrigeration cycle apparatus using the refrigerant R410A. The amount of refrigerant (upper limit value and lower limit value) sealed in the refrigeration cycle apparatus using the refrigerant R32 will be described with reference to FIG.

 図4は、冷媒R32を使用した冷凍サイクル装置において、冷媒R410Aを使用した冷凍サイクル装置と同等のCOPとなる冷媒量比の関係を示しており、横軸は定格冷凍能力、縦軸はR410Aの冷媒量を基準とした冷媒量比である。また、この図4は、上述した図2及び図3に示したCOPが同等となる冷媒量比をプロットした線図である。プロットした点を結んだ直線は、冷媒R410Aを使用した冷凍サイクル装置のCOPと同一とするために必要な冷媒量比の下限値を示している。 FIG. 4 shows the relationship between the refrigerant amount ratios in the refrigeration cycle apparatus using the refrigerant R32 and a COP equivalent to that of the refrigeration cycle apparatus using the refrigerant R410A. The horizontal axis represents the rated refrigeration capacity, and the vertical axis represents the R410A. The refrigerant amount ratio is based on the refrigerant amount. Further, FIG. 4 is a diagram in which the refrigerant amount ratio in which the COPs shown in FIGS. 2 and 3 described above are equivalent is plotted. A straight line connecting the plotted points indicates the lower limit value of the refrigerant amount ratio necessary to be the same as the COP of the refrigeration cycle apparatus using the refrigerant R410A.

 ここで、冷媒R32を使用した冷凍サイクル装置の接続配管7,8の管外径は、定格冷凍能力7.1kW以上では、前記「(Do-1)/8インチ」(例えば、ガス側接続配管径は4/8インチ、液側接続配管径は2/8インチ)に設定され、また、定格冷凍能力7.1kW未満では、ガス側接続配管8は前記「(Do-1)/8インチ」(例えば、3/8インチ)、液側接続配管7では前記「(Do-1)/16インチ」(例えば、3/16インチ)に設定されている。 Here, the pipe outer diameter of the connection pipes 7 and 8 of the refrigeration cycle apparatus using the refrigerant R32 is “(D o −1) / 8 inch” (for example, gas side connection) when the rated refrigeration capacity is 7.1 kW or more. The pipe diameter is set to 4/8 inch, and the liquid side connection pipe diameter is set to 2/8 inch). When the rated refrigeration capacity is less than 7.1 kW, the gas side connection pipe 8 is the “(D o −1) / 8”. Inch ”(for example, 3/8 inch), and“ (D o −1) / 16 inch ”(for example, 3/16 inch) in the liquid side connection pipe 7 is set.

 定格冷凍能力Qc[kW]の冷媒R32を使用した冷凍サイクル装置に封入する冷媒量をW1[kg]、定格冷凍能力Qc[kW]の冷媒R410Aを使用した冷凍サイクル装置の冷媒量W0[kg]としたとき、前記冷媒量比をGRとすると、冷媒量比をGRは次式で定義される。 
   GR=W1/W0
 また、定格冷凍能力Qc[kW]の冷媒R32を使用した冷凍サイクル装置に封入する冷媒量W1[kg]は、次式で表すことができる。 
   W1=GR・W0
 R32を使用した冷凍サイクル装置での接続配管7,8の管外径を前記「(Do-1)/8インチ」に設定する場合は、図4の定格冷凍能力7.1kW以上における冷媒量比を結んだ直線(太線)に相当し、その冷媒量比GRの下限値をGRmAとすると、図4から、
   GRmA=0.011Qc+0.60
で表すことができる。従って、冷媒R32を使用した冷凍サイクル装置の冷媒量の下限値をW1mA[kg]とすると、
   W1mA=GRmA・W0=(0.011Qc+0.60)W0[kg]
で表すことができる。
The refrigerant amount W 1 [kg] to be sealed in the refrigeration cycle apparatus using the refrigerant R32 having the rated refrigeration capacity Qc [kW] is W 1 [kg], and the refrigerant quantity W 0 of the refrigeration cycle apparatus using the refrigerant R410A having the rated refrigeration capacity Qc [kW]. when a kg], when the refrigerant amount ratio and G R, the refrigerant amount ratio G R is defined by the following equation.
G R = W 1 / W 0
The refrigerant amount W 1 sealed in a refrigeration cycle apparatus using the refrigerant R32 rated cooling capacity Qc [kW] [kg] can be expressed by the following equation.
W 1 = G R · W 0
When the pipe outer diameters of the connection pipes 7 and 8 in the refrigeration cycle apparatus using R32 are set to “(D o −1) / 8 inch”, the refrigerant amount at the rated refrigeration capacity of 7.1 kW or more in FIG. corresponds to the connecting ratio line (thick line), when the lower limit of the refrigerant amount ratio G R and G RMA, from FIG. 4,
G RmA = 0.011Qc + 0.60
Can be expressed as Therefore, if the lower limit value of the refrigerant amount of the refrigeration cycle apparatus using the refrigerant R32 is W 1 mA [kg],
W 1mA = G RmA · W 0 = (0.011Qc + 0.60) W 0 [kg]
Can be expressed as

 次に、R32を使用した冷凍サイクル装置での接続配管7,8の管外径を、ガス側接続配管8では前記「(Do-1)/8インチ」に設定し、液側接続配管7では前記「(Do-1)/16インチ」に設定する場合は、図4の定格冷凍能力7.1kW未満における冷媒量比を結んだ直線(細線)に相当し、その冷媒量比の下限値をGRmBとすると、図4から、
   GRmB=0.030Qc+0.71
で表すことができる。従って、冷媒R32を使用した冷凍サイクル装置の冷媒量の下限値をW1mB[kg]とすると、
   W1mB=GRmB・W0=(0.030Qc+0.71)W0[kg]
で表すことができる。
Next, the pipe outer diameter of the connection pipes 7 and 8 in the refrigeration cycle apparatus using R32 is set to the “(D o −1) / 8 inch” in the gas side connection pipe 8, and the liquid side connection pipe 7 Then, when setting to “(D o −1) / 16 inch”, it corresponds to the straight line (thin line) connecting the refrigerant amount ratios at the rated refrigeration capacity of less than 7.1 kW in FIG. 4, and the lower limit of the refrigerant amount ratio If the value is G RmB , from FIG.
G RmB = 0.030Qc + 0.71
Can be expressed as Therefore, when the lower limit value of the refrigerant amount of the refrigeration cycle apparatus using the refrigerant R32 is W 1 mB [kg],
W 1mB = G RmB · W 0 = (0.030Qc + 0.71) W 0 [kg]
Can be expressed as

 以上説明したように、冷媒R32を使用した冷凍サイクル装置での接続配管7,8の管外径を前記「(Do-1)/8インチ」に設定する場合は、冷媒量の下限値を「(0.011Qc+0.60)W0[kg]」に設定することにより、冷凍サイクル装置の性能低下を生じさせることなく、冷媒を冷媒R410Aから冷媒R32に転換することができる。しかも、冷媒R410A使用の冷凍サイクル装置に比べて冷媒封入量を低減可能な冷凍サイクル装置を得ることが可能になる。 As described above, when the pipe outer diameters of the connection pipes 7 and 8 in the refrigeration cycle apparatus using the refrigerant R32 are set to “(D o −1) / 8 inch”, the lower limit value of the refrigerant amount is set to By setting to “(0.011Qc + 0.60) W 0 [kg]”, the refrigerant can be converted from the refrigerant R410A to the refrigerant R32 without causing the performance of the refrigeration cycle apparatus to deteriorate. In addition, it is possible to obtain a refrigeration cycle apparatus that can reduce the amount of refrigerant enclosed as compared with the refrigeration cycle apparatus using the refrigerant R410A.

 また、冷媒R32を使用した冷凍サイクル装置での接続配管7,8の管外径を定格冷凍能力によって分ける場合には次のようにする。 
 定格冷凍能力が7.1kW以上では、接続配管7,8の管外径を前記「(Do-1)/8インチ」に設定し、このときの冷媒量の下限値を「(0.011Qc+0.60)W0[kg]」に設定する。
Further, when the pipe outer diameters of the connection pipes 7 and 8 in the refrigeration cycle apparatus using the refrigerant R32 are divided according to the rated refrigeration capacity, the following is performed.
When the rated refrigeration capacity is 7.1 kW or more, the pipe outer diameters of the connection pipes 7 and 8 are set to “(D o −1) / 8 inch”, and the lower limit value of the refrigerant amount at this time is set to “(0.011Qc + 0 .60) W 0 [kg] ”.

 また、定格冷凍能力7.1kW未満では、ガス側接続配管8では前記「(Do-1)/8インチ」に、液側接続配管7では前記「(Do-1)/16インチ」に設定する。 In addition, when the rated refrigeration capacity is less than 7.1 kW, the gas side connection pipe 8 is the “(D o −1) / 8 inch”, and the liquid side connection pipe 7 is the “(D o −1) / 16 inch”. Set.

 そして、冷媒量の下限値を「(0.030Qc+0.71)W0[kg]」に設定することで、冷媒を冷媒R410Aから冷媒R32に転換した際に冷凍サイクル装置の性能低下を生じさせることなく、冷媒R410Aを使用した冷凍サイクル装置に比べて冷媒封入量を低減可能な冷凍サイクル装置を得ることが可能になる。 Then, by setting the lower limit value of the refrigerant amount to “(0.030Qc + 0.71) W 0 [kg]”, when the refrigerant is changed from the refrigerant R410A to the refrigerant R32, the performance of the refrigeration cycle apparatus is deteriorated. As a result, it is possible to obtain a refrigeration cycle apparatus capable of reducing the amount of refrigerant enclosed as compared with the refrigeration cycle apparatus using the refrigerant R410A.

 図5は冷媒R32を使用した冷凍サイクル装置と冷媒R410Aを使用した冷凍サイクル装置の冷媒量を同一に設定した場合の冷媒R32を使用した冷凍サイクル装置の冷媒R410Aを使用した冷凍サイクル装置を基準としたCOP比を示している。また、この図5には使用される接続配管径も表示されている。 FIG. 5 is based on the refrigeration cycle apparatus using the refrigerant R410A of the refrigeration cycle apparatus using the refrigerant R32 when the refrigerant amount of the refrigeration cycle apparatus using the refrigerant R32 and the refrigeration cycle apparatus using the refrigerant R410A are set to be the same. The COP ratio is shown. Further, FIG. 5 also shows the connection pipe diameter used.

 この図5に示したCOP比は、前記接続配管7,8の長さが短接続配管(定格冷凍能力3.6kW及び5.6kWのものでは5m、定格冷凍能力7.1kW及び12.5kWのものでは7.5m)に設定された場合のものである。 The COP ratio shown in FIG. 5 is that the lengths of the connecting pipes 7 and 8 are short connecting pipes (5 m for rated refrigeration capacities of 3.6 kW and 5.6 kW, rated refrigeration capacities of 7.1 kW and 12.5 kW). In the case of a thing, it is a thing when set to 7.5 m).

 この図5から、冷媒R32を使用した冷凍サイクル装置での冷媒量が、冷媒R410Aを使用した冷凍サイクル装置と同一(冷媒量比1.0)とした場合には、冷媒R32を使用した冷凍サイクル装置のCOPを、冷媒R410Aを使用した冷凍サイクル装置のCOPに対して同等以上のCOPにすることが可能である。 From FIG. 5, when the refrigerant amount in the refrigeration cycle apparatus using the refrigerant R32 is the same as that of the refrigeration cycle apparatus using the refrigerant R410A (refrigerant amount ratio 1.0), the refrigeration cycle using the refrigerant R32 is used. The COP of the apparatus can be equal to or higher than the COP of the refrigeration cycle apparatus using the refrigerant R410A.

 以上のことから、接続配管7,8の配管長が、短配管長からチャージレス最大配管長の間において、冷媒R410Aを使用した冷凍サイクル装置の冷媒封入量よりも少なく設定することができる。また、性能向上を図る場合には、前述した冷媒量の下限値W1mA、W1mB以上で、冷媒R32を使用した冷凍サイクル装置の定格冷凍能力Qc[kW]と同じ定格冷凍能力の冷媒R410Aを使用した冷凍サイクル装置の冷媒量W0[kg]未満に設定すると良い。 From the above, the pipe lengths of the connection pipes 7 and 8 can be set to be smaller than the refrigerant charging amount of the refrigeration cycle apparatus using the refrigerant R410A between the short pipe length and the maximum chargeless pipe length. In order to improve the performance, the refrigerant R410A having the same rated refrigeration capacity as the rated refrigeration capacity Qc [kW] of the refrigeration cycle apparatus using the refrigerant R32 at the lower limit values W 1mA and W 1mB of the refrigerant amount described above is used. It may be set to less than the refrigerant amount W 0 [kg] of the used refrigeration cycle apparatus.

 なお、この実施例2においても、冷凍サイクル装置は図1に示したものと同様のものを使用しており、特に言及していない部分については実施例1に示したものと同様の構成となっている。 In the second embodiment, the refrigeration cycle apparatus is the same as that shown in FIG. 1, and the parts not particularly mentioned have the same configuration as that shown in the first embodiment. ing.

 以上述べたように、本実施例によれば、冷媒R32を使用した冷凍サイクル装置にすると共に、接続配管径を、従来の冷媒R410Aを使用した冷凍サイクル装置よりも細径に設定するようにしているので、冷媒R410Aを使用した従来の冷凍サイクル装置よりも冷凍サイクル内に封入する冷媒量を低減でき、また前記接続配管の材料である銅の使用量も削減することが可能となる。更に、接続配管径を細径にすることにより、銅の使用量の削減だけでなく、冷凍空調機器(冷凍サイクル装置)施工時の接続配管の施工性を向上することもできる。また、低GWP冷媒であるR32を使用しているので、地球温暖化防止にも有効である。 As described above, according to the present embodiment, the refrigeration cycle apparatus using the refrigerant R32 is used, and the connection pipe diameter is set to be smaller than that of the conventional refrigeration cycle apparatus using the refrigerant R410A. Therefore, the amount of refrigerant sealed in the refrigeration cycle can be reduced as compared with the conventional refrigeration cycle apparatus using the refrigerant R410A, and the amount of copper used as the material for the connection pipe can be reduced. Furthermore, by reducing the diameter of the connecting pipe, not only the amount of copper used can be reduced, but also the workability of the connecting pipe at the time of construction of the refrigeration air conditioner (refrigeration cycle apparatus) can be improved. Moreover, since R32 which is a low GWP refrigerant | coolant is used, it is effective also in global warming prevention.

 更に、冷媒R32を使用した冷凍サイクル装置に封入する冷媒量の範囲を、図4に示した太線或いは細線に基づいて求めた冷媒量より多く、冷媒R410Aを使用した従来の冷凍サイクル装置における冷媒封入量よりも少なくすることで、COPの高い冷凍サイクル装置を得ることも可能となる。 Furthermore, the range of the refrigerant amount sealed in the refrigeration cycle apparatus using the refrigerant R32 is larger than the refrigerant quantity obtained based on the thick line or the thin line shown in FIG. 4, and the refrigerant enclosure in the conventional refrigeration cycle apparatus using the refrigerant R410A is performed. By reducing the amount, the refrigeration cycle apparatus having a high COP can be obtained.

 このように本実施例によれば、地球温暖化係数(GWP)の低い冷媒を使用しつつ効率低下を抑制し、しかも接続配管の配管径も小さくすることのできる冷凍サイクル装置を得ることができる効果が得られる。 As described above, according to the present embodiment, it is possible to obtain a refrigeration cycle apparatus that can suppress a decrease in efficiency while using a refrigerant having a low global warming potential (GWP) and that can also reduce the pipe diameter of the connection pipe. An effect is obtained.

1…圧縮機、
2…四方弁、
3…熱源機側熱交換器、
4…第1の膨張装置、21…第2の膨張装置、
6,9…阻止弁、
7…液側接続配管、8…ガス側接続配管、
10…アキュムレータ、
20…室内機、
22…利用側熱交換器、
40…室外機。
1 ... Compressor,
2 ... Four-way valve,
3. Heat source machine side heat exchanger,
4 ... 1st expansion device, 21 ... 2nd expansion device,
6, 9 ... Stop valve,
7 ... Liquid side connection piping, 8 ... Gas side connection piping,
10 ... Accumulator,
20 ... indoor unit,
22 ... Use side heat exchanger,
40 ... Outdoor unit.

Claims (7)

 圧縮機、熱源機側熱交換器、第1の膨張装置、液側接続配管、第2の膨張装置、利用側熱交換器、ガス側接続配管を順次接続して構成されている冷凍サイクル装置において、
 前記冷凍サイクルに使用する冷媒をR32とし、
 前記液側接続配管と、前記ガス側接続配管の管外径を、
   (D0-1)/8インチ
(ここで、「D0/8インチ」は冷媒R410Aを使用した場合の接続配管外径である)とし、且つ前記液接続配管では前記D0の範囲を「2≦D0≦4」とし、前記ガス接続配管では前記D0の範囲を「3≦D0≦8」とした
 ことを特徴とする冷凍サイクル装置。
In a refrigeration cycle apparatus configured by sequentially connecting a compressor, a heat source machine side heat exchanger, a first expansion device, a liquid side connection pipe, a second expansion device, a use side heat exchanger, and a gas side connection pipe ,
The refrigerant used in the refrigeration cycle is R32,
Pipe outer diameters of the liquid side connection pipe and the gas side connection pipe are:
(D 0 -1) / 8 inches (where "D 0/8 inches" is a connection pipe outer diameter in the case of using the refrigerant R410A) and, and the range of the D 0 in the liquid connection pipe " 2 ≦ D 0 ≦ 4 ”, and in the gas connection pipe, the range of D 0 is“ 3 ≦ D 0 ≦ 8 ”.
 請求項1に記載の冷凍サイクル装置において、
 定格冷凍能力が7.1kWから12.5kWまでの範囲では、前記液接続配管では前記D0を3(即ち配管径が1/4インチ)、前記ガス接続配管では前記D0を5(即ち配管径が1/2インチ)とし、
 定格冷凍能力が3.6kWから7.1kW未満の範囲では、前記液接続配管では前記D0を2.5(即ち配管径が3/16インチ)、前記ガス側接続配管では前記D0を4(即ち配管径が3/8インチ)とした
 ことを特徴とする冷凍サイクル装置。
The refrigeration cycle apparatus according to claim 1,
In the range of the rated cooling capacity from 7.1kW up to 12.5kW, the D 0 to 3 (i.e. a pipe diameter of 1/4 inch) in the liquid connection pipe, the D 0 is the gas connection pipe 5 (i.e. piping The diameter is 1/2 inch)
When the rated refrigeration capacity is in the range of 3.6 kW to less than 7.1 kW, D 0 is 2.5 (that is, the pipe diameter is 3/16 inch) in the liquid connection pipe, and D 0 is 4 in the gas side connection pipe. (That is, the pipe diameter is 3/8 inch).
 圧縮機、熱源機側熱交換器、第1の膨張装置、液側接続配管、第2の膨張装置、利用側熱交換器、ガス側接続配管を順次接続して構成されている冷凍サイクル装置において、
 前記冷凍サイクルに使用する冷媒をR32とし、
 前記液側接続配管と、前記ガス側接続配管の管外径を、
   D0/8インチ
とし、且つ前記液接続配管では前記D0の範囲を「1≦D0≦3」とし、前記ガス接続配管では前記D0の範囲を「2≦D0≦7」とした
 ことを特徴とする冷凍サイクル装置。
In a refrigeration cycle apparatus configured by sequentially connecting a compressor, a heat source machine side heat exchanger, a first expansion device, a liquid side connection pipe, a second expansion device, a use side heat exchanger, and a gas side connection pipe ,
The refrigerant used in the refrigeration cycle is R32,
Pipe outer diameters of the liquid side connection pipe and the gas side connection pipe are:
D 0/8 inches, and in the liquid connection pipe, the range of D 0 is “1 ≦ D 0 ≦ 3”, and in the gas connection pipe, the range of D 0 is “2 ≦ D 0 ≦ 7”. A refrigeration cycle apparatus characterized by that.
 請求項3に記載の冷凍サイクル装置において、
 定格冷凍能力が7.1kWから12.5kWまでの範囲では、前記液接続配管では前記D0を2(即ち配管径が1/4インチ)、前記ガス接続配管では前記D0を4(即ち配管径が1/2インチ)とし、
 定格冷凍能力が3.6kWから7.1kW未満の範囲では、前記液接続配管では前記D0を1.5(即ち配管径が3/16インチ)、前記ガス側接続配管では前記D0を3(即ち配管径が3/8インチ)とした
 ことを特徴とする冷凍サイクル装置。
The refrigeration cycle apparatus according to claim 3,
In the range from the rated cooling capacity is 7.1kW up to 12.5kW, the D 0 to 2 (i.e., the pipe diameter of 1/4 inch) in the liquid connection piping, 4 the D 0 in the gas connection pipe (i.e. the pipe The diameter is 1/2 inch)
When the rated refrigeration capacity is in the range of 3.6 kW to less than 7.1 kW, the D 0 is 1.5 (that is, the pipe diameter is 3/16 inch) in the liquid connection pipe, and the D 0 is 3 in the gas side connection pipe. (That is, the pipe diameter is 3/8 inch).
 請求項1~4の何れかに記載の冷凍サイクル装置において、
 冷凍サイクル装置への冷媒R32の封入量を、冷媒としてR410Aを使用し且つ定格冷凍能力が同一で同一仕様の冷凍サイクル装置に封入している冷媒R410Aの封入量よりも少ない封入量に設定している
 ことを特徴とする冷凍サイクル装置。
The refrigeration cycle apparatus according to any one of claims 1 to 4,
The amount of refrigerant R32 enclosed in the refrigeration cycle apparatus is set to an amount smaller than the amount of refrigerant R410A enclosed in the refrigeration cycle apparatus of the same specification that uses R410A as the refrigerant and has the same rated refrigeration capacity. A refrigeration cycle apparatus characterized by comprising:
 請求項5に記載の冷凍サイクル装置において、
 冷凍サイクル装置への冷媒R32の封入量をW1[kg]、前記冷凍サイクル装置の定格冷凍能力をQc[kW]、冷媒R410Aを使用した同一の定格冷凍能力Qc[kW]の冷凍サイクル装置における冷媒封入量をW0[kg]としたとき、前記冷媒R32を使用した前記冷凍サイクル装置への前記冷媒封入量W1を、
   (0.011Qc+0.60)W0≦W1<W0
の範囲に設定している
 ことを特徴とする冷凍サイクル装置。
The refrigeration cycle apparatus according to claim 5,
In the refrigeration cycle apparatus having the same rated refrigeration capacity Qc [kW] using the refrigerant R32A, the amount of refrigerant R32 enclosed in the refrigeration cycle apparatus is W 1 [kg], the rated refrigeration capacity of the refrigeration cycle apparatus is Qc [kW], and the refrigerant R410A is used. When the refrigerant charging amount is W 0 [kg], the refrigerant charging amount W 1 to the refrigeration cycle apparatus using the refrigerant R32 is
(0.011Qc + 0.60) W 0 ≦ W 1 <W 0
The refrigeration cycle apparatus is characterized by being set in the range of.
 請求項5に記載の冷凍サイクル装置において、
 冷凍サイクル装置への冷媒R32の封入量をW1[kg]、前記冷凍サイクル装置の定格冷凍能力をQc[kW]、冷媒R410Aを使用した同一の定格冷凍能力Qc[kW]の冷凍サイクル装置における冷媒封入量をW0[kg]としたとき、前記冷媒R32を使用した前記冷凍サイクル装置への前記冷媒封入量W1を、
 Qc≧7.1kWでは、
   (0.011Qc+0.60)W0≦W1<W0
 Qc<7.1kWでは、
   (0.030Qc+0.71)W0≦W1<W0
の範囲に設定している
 ことを特徴とする冷凍サイクル装置。
The refrigeration cycle apparatus according to claim 5,
In the refrigeration cycle apparatus having the same rated refrigeration capacity Qc [kW] using the refrigerant R32A, the amount of refrigerant R32 enclosed in the refrigeration cycle apparatus is W 1 [kg], the rated refrigeration capacity of the refrigeration cycle apparatus is Qc [kW], and the refrigerant R410A is used. When the refrigerant charging amount is W 0 [kg], the refrigerant charging amount W 1 to the refrigeration cycle apparatus using the refrigerant R32 is
For Qc ≧ 7.1 kW,
(0.011Qc + 0.60) W 0 ≦ W 1 <W 0
For Qc <7.1 kW,
(0.030Qc + 0.71) W 0 ≦ W 1 <W 0
The refrigeration cycle apparatus is characterized by being set in the range of.
PCT/JP2013/055773 2012-03-26 2013-03-04 Refrigerating cycle device Ceased WO2013146103A1 (en)

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JP5536817B2 (en) 2014-07-02
EP2840335A1 (en) 2015-02-25
CN104094069B (en) 2016-02-03
US20140373569A1 (en) 2014-12-25
JP2013200090A (en) 2013-10-03
EP2840335A4 (en) 2016-01-20
US10066859B2 (en) 2018-09-04
CN104094069A (en) 2014-10-08
EP2840335B1 (en) 2022-05-04

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